CN202643350U - Urea low-pressure deep hydrolysis waste liquor recovery device - Google Patents

Urea low-pressure deep hydrolysis waste liquor recovery device Download PDF

Info

Publication number
CN202643350U
CN202643350U CN 201220245555 CN201220245555U CN202643350U CN 202643350 U CN202643350 U CN 202643350U CN 201220245555 CN201220245555 CN 201220245555 CN 201220245555 U CN201220245555 U CN 201220245555U CN 202643350 U CN202643350 U CN 202643350U
Authority
CN
China
Prior art keywords
storage tank
waste liquor
waste
hydrolysis
pipeline
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 201220245555
Other languages
Chinese (zh)
Inventor
张少峰
薛艳军
许会宗
伍革卫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LINGBAO XINGHUA CHEMICAL Industry Co Ltd
Original Assignee
LINGBAO XINGHUA CHEMICAL Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LINGBAO XINGHUA CHEMICAL Industry Co Ltd filed Critical LINGBAO XINGHUA CHEMICAL Industry Co Ltd
Priority to CN 201220245555 priority Critical patent/CN202643350U/en
Application granted granted Critical
Publication of CN202643350U publication Critical patent/CN202643350U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The utility model provides a urea low-pressure deep hydrolysis waste liquor recovery device. The device comprises a hydrolysis waste liquor storage tank, wherein the inlet of the hydrolysis waste liquor storage tank is connected with a hydrolysis waste liquor discharge pipeline; the hydrolysis waste liquor storage tank is connected with a chemical feed storage tank through a pipeline and a delivery pump; the outlet of the chemical feed storage tank is connected with the hydrolysis waste liquor storage tank through a pipeline; the pipeline of the outlet of the delivery pump is provided with a waste liquor discharge port for delivering waste liquor to a gas making section; and a chemical feed port is formed on the top of the chemical feed storage tank. The urea low-pressure deep hydrolysis waste liquor recovery device is simple in structure and practical in functions, and can be used for sufficiently recovering waste water generated by low-pressure deep hydrolysis of urea production, so that the cost for discharging waste water can be reduced, gas-making desalted water consumption can be reduced, environmental pollution or equipment corrosion caused by other waste water treatments can be eliminated.

Description

Urea depth of depression waste hydrolyzed liquid retrieving arrangement
Technical field
The utility model relates to a kind of urea depth of depression waste hydrolyzed liquid retrieving arrangement.
Background technology
Existing urea depth of depression waste hydrolyzed liquid or directly discharging or be recycled to the gas making utilization.And the environmental pollution that the direct discharging of waste liquid causes brings larger environmental protection pressure to enterprise, or recycle but because the low not treated direct utilization of urea production waste water PH after the depth of depression hydrolysis treatment then easily causes corrosion to equipment, affect the For Gas-making Process life of equipment.
The utility model content
The utility model provides a kind of urea depth of depression waste hydrolyzed liquid retrieving arrangement, simple in structure, safe and reliable to operation, do not increase urea and the consumption of For Gas-making Process economy, and minimizing waste water effluxes the generation expense, and reduce the consumption of gas making de-salted water, eliminate the environmental pollution that other wastewater treatment causes or cause equipment corrosion.
In order to solve the problems of the technologies described above, the utility model adopts following technical scheme: urea depth of depression waste hydrolyzed liquid retrieving arrangement, comprise the waste hydrolyzed liquid storage tank, the import of waste hydrolyzed liquid storage tank is connected with the hydrolysis waste solution channel, the waste hydrolyzed liquid storage tank by pipeline be connected pump outside and be connected with the dosing storage tank, the outlet of dosing storage tank is connected with the waste hydrolyzed liquid storage tank by pipeline, is provided with at the pipeline of sending pump outlet outside waste liquid is sent to the waste liquid relief outlet that For Gas-making Process uses.
The dosing tank top is provided with dosing mouth.
Simple in structure, the practical function of the utility model, fully reclaimed the waste water that the hydrolysis of urea production depth of depression produces, reduced waste water and efflux the generation expense, and reduce the consumption of gas making de-salted water, eliminate the environmental pollution that other wastewater treatment causes, or cause equipment corrosion.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Embodiment: as shown in Figure 1, urea depth of depression waste hydrolyzed liquid retrieving arrangement, comprise waste hydrolyzed liquid storage tank 2,2 imports of waste hydrolyzed liquid storage tank are connected with hydrolysis waste solution channel 1, waste hydrolyzed liquid storage tank 2 by pipeline be connected pump 3 outside and be connected with dosing storage tank 4, the outlet of dosing storage tank 4 is connected with waste hydrolyzed liquid storage tank 2 by pipeline, is provided with at the pipeline of the outlet of sending pump 3 outside waste liquid is sent to the waste liquid relief outlet 5 that For Gas-making Process uses.Dosing storage tank 4 tops are provided with dosing mouth.
The utility model enters waste hydrolyzed liquid storage tank 2 at the waste liquor stream that the depth of depression hydrolysis produces, and after processing through dosing, delivers to the For Gas-making Process utilization after sending pump 3 pressurizations outside.Dosing storage tank 4 needs regularly to add inhibiter, and by after sending pump 3 outside and introducing waste liquids inhibiter is dissolved, the control flow utilizes potential difference automatically to flow into waste liquid and reclaims storage tank and waste liquid is carried out dosing process, and control is sent the waste liquid pH value outside and reduced corrosion.

Claims (2)

1. urea depth of depression waste hydrolyzed liquid retrieving arrangement, it is characterized in that: comprise the waste hydrolyzed liquid storage tank, the import of waste hydrolyzed liquid storage tank is connected with the hydrolysis waste solution channel, the waste hydrolyzed liquid storage tank by pipeline be connected pump outside and be connected with the dosing storage tank, the outlet of dosing storage tank is connected with the waste hydrolyzed liquid storage tank by pipeline, is provided with at the pipeline of sending pump outlet outside waste liquid is sent to the waste liquid relief outlet that For Gas-making Process uses.
2. urea depth of depression waste hydrolyzed liquid retrieving arrangement according to claim 1, it is characterized in that: the dosing tank top is provided with dosing mouth.
CN 201220245555 2012-05-29 2012-05-29 Urea low-pressure deep hydrolysis waste liquor recovery device Expired - Fee Related CN202643350U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220245555 CN202643350U (en) 2012-05-29 2012-05-29 Urea low-pressure deep hydrolysis waste liquor recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220245555 CN202643350U (en) 2012-05-29 2012-05-29 Urea low-pressure deep hydrolysis waste liquor recovery device

Publications (1)

Publication Number Publication Date
CN202643350U true CN202643350U (en) 2013-01-02

Family

ID=47412487

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220245555 Expired - Fee Related CN202643350U (en) 2012-05-29 2012-05-29 Urea low-pressure deep hydrolysis waste liquor recovery device

Country Status (1)

Country Link
CN (1) CN202643350U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111995105A (en) * 2020-07-22 2020-11-27 华南理工大学 Urea desorption waste liquid ammonia nitrogen emission reduction and waste water recycling equipment and use method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111995105A (en) * 2020-07-22 2020-11-27 华南理工大学 Urea desorption waste liquid ammonia nitrogen emission reduction and waste water recycling equipment and use method

Similar Documents

Publication Publication Date Title
CN102886199B (en) Flue gas desulfurization device and desulfurization method by magnesium oxide process
CN204237619U (en) A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor
CN202151529U (en) Recycling device for titanium white postprocessing washing liquid
CN202643350U (en) Urea low-pressure deep hydrolysis waste liquor recovery device
CN202022925U (en) Device for pressurizing, backflowing, shell breaking and stirring methane liquid at bottom layer of methane tank
CN204569680U (en) A kind of waste disposal plant
CN102583932A (en) Method for generating methane by enhancing anaerobic digestion of reflux sludge after heat and alkaoline combined treatment and circulation
CN213171587U (en) Novel reverse osmosis unit antisludging agent intelligence charge system
CN204554775U (en) Boiler blow-off apparatus for recovering
CN204958571U (en) Coking wastewater nanofiltration concentrate processing apparatus
CN207347349U (en) A kind of Circulating Cooling Water of Power Plant blowdown reclaiming system
CN201372239Y (en) Reverse osmosis concentrate reusing device
CN205035186U (en) System for retrieve promoter M in follow promoter CBS waste liquid
CN213574877U (en) Vacuum pump tank combination
CN202558657U (en) Waste water recycle device in antibiotic fermentation system
CN204778891U (en) Ferment waste water recycle device before yellow rice wine
CN204803134U (en) Professional equipment of online resourceful treatment technology of gasification buck
CN203021313U (en) System for recycling waste water after ink production
CN204939129U (en) The safe blue algae water treatment unit of pressure type
CN203256182U (en) Extraction and recovering device for intermediate
CN202717647U (en) Recovering treatment system of copper and chromium in electroplating wastewater
CN204661399U (en) A kind of high-concentration organic wastewater treatment device water feed apparatus
CN202849185U (en) Circulating water recycling device
CN204185317U (en) A kind of Fenton advanced oxidation system for the treatment of refuse percolate
CN204034515U (en) A kind of hydrogen chloride tail gas recovery device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130102

Termination date: 20160529